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Catalyst for selective hydrogenation of acetylene compounds in 1,3-butadiene, method for producing the same and method of using the same

An alkyne compound, selective hydrogenation technology, applied in metal/metal oxide/metal hydroxide catalyst, catalyst activation/preparation, physical/chemical process catalyst, etc., can solve the problem of lack of selectivity

Inactive Publication Date: 2011-08-24
SUD CHEM CATALYSTS JAPAN
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, although the elution of Pd is suppressed, there is no description about the improvement of its selectivity.
That is, none of the existing technologies can maintain the activity of palladium-based catalysts for the selective hydrogenation of C4 alkyne compounds at a high level, and at the same time, no problems caused by overhydrogenation will occur at the level of selectivity. Complete removal of C4 alkynes under the premise of loss of 1,3-butadiene

Method used

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  • Catalyst for selective hydrogenation of acetylene compounds in 1,3-butadiene, method for producing the same and method of using the same
  • Catalyst for selective hydrogenation of acetylene compounds in 1,3-butadiene, method for producing the same and method of using the same
  • Catalyst for selective hydrogenation of acetylene compounds in 1,3-butadiene, method for producing the same and method of using the same

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] Add 18.3ml of palladium chloride solution (120g / L) into 1200ml of pure water, add 1000g of alumina carrier therein, leave it for 90 minutes, remove the solution, reduce it with 5% sodium formate solution at 60°C, wash it with water, Dry in air to obtain a Pd catalyst. On the other hand, 4.3 g of bismuth nitrate was completely dissolved in a solution obtained by adding 15 ml of concentrated nitric acid to 165 ml of pure water, and this solution was added to a Pd catalyst (300 g), followed by firing at 500°C. After calcining, the catalyst was obtained by reduction in hydrogen at 350°C. The composition ratio of this catalyst was Pd / Bi=0.2% / 0.6%.

[0038] The catalyst was measured with an XRD measuring device. Copper was used for the cathode, and the measurement was performed at an output of 40 mA and 45 kV at a wavelength of 1.54 angstroms. The results are shown in Fig. 1(a). There is a peak around 2θ=28°, which is not seen in FIG. 1(b) showing the peak of the catalyst...

Embodiment 2

[0040] The Pd catalyst was obtained by the same method as in Example 1. On the other hand, 2.9 g of bismuth nitrate was completely dissolved in a solution obtained by adding 10 ml of concentrated nitric acid to 170 ml of pure water. After adding this solution to a Pd catalyst (300 g), it baked at 500 degreeC. After firing, it is reduced in hydrogen at 350°C to obtain a catalyst. The composition ratio of this catalyst was Pd / Bi=0.2% / 0.4%.

Embodiment 3

[0042] The Pd catalyst was obtained by the same method as in Example 1. On the other hand, 5.6 g of bismuth nitrate was completely dissolved in a solution obtained by adding 20 ml of concentrated nitric acid to 160 ml of pure water. After adding this solution to a Pd catalyst (300 g), it baked at 500 degreeC. After firing, it is reduced in hydrogen at 350°C to obtain a catalyst. The composition ratio of this catalyst was Pd / Bi=0.2% / 0.8%.

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PUM

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Abstract

It is intended to provide a catalyst for selective hydrogenation to be used in a process for obtaining 1,3-butadiene by selectively hydrogenating acetylene compounds contained in a C4 hydrocarbon compound reservoir obtained by steam cracking and mainly containing 1,3-butadiene. The catalyst has a composition mainly containing palladium and bismuth, or palladium, bismuth, and tellurium.

Description

technical field [0001] The present invention relates to a method suitable for the selective hydrogenation of acetylenic compounds contained in a C4 hydrocarbon fraction (Japanese: 混) mainly containing 1,3-butadiene to obtain high-purity 1,3-butadiene Catalyst for the reaction, method for producing the same, and method for using the same. Background technique [0002] Various olefin compounds, which are basic raw materials in the petrochemical industry, are usually produced by steam cracking of naphtha, but contain highly unsaturated hydrocarbons, which must be removed in order to be used as raw materials for the polymer chemical industry. For the manufacture of olefinic compounds such as ethylene, propylene, butadiene, isoprene, and the like, useful materials such as ethylene, propylene, butenes, butadiene, isoprene in the feed stream And the loss of other same materials is minimized, it is necessary to remove the alkyne impurities in various unrefined mixed C2~C5 compound ...

Claims

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Application Information

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IPC IPC(8): B01J23/644C07C5/09C07C7/167C07C11/167C07B61/00
CPCB01J35/008B01J23/6447B01J37/18C07C7/167B01J23/002B01J27/0576B01J37/0205B01J2523/00B01J37/16B01J35/397B01J2523/54B01J2523/64B01J2523/824C07C11/167B01J23/644B01J27/057C07C5/09
Inventor 菅田守保深田博史
Owner SUD CHEM CATALYSTS JAPAN